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EP0003230A2 - Process for the preparation of o-phthalic aldehydes optionally having several substituents - Google Patents

Process for the preparation of o-phthalic aldehydes optionally having several substituents Download PDF

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Publication number
EP0003230A2
EP0003230A2 EP78101723A EP78101723A EP0003230A2 EP 0003230 A2 EP0003230 A2 EP 0003230A2 EP 78101723 A EP78101723 A EP 78101723A EP 78101723 A EP78101723 A EP 78101723A EP 0003230 A2 EP0003230 A2 EP 0003230A2
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alkaline earth
hydrolysis
alkali metal
earth metal
carries out
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EP0003230B1 (en
EP0003230A3 (en
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Jacques Dr. Gosteli
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Novartis AG
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Ciba Geigy AG
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C201/00Preparation of esters of nitric or nitrous acid or of compounds containing nitro or nitroso groups bound to a carbon skeleton
    • C07C201/06Preparation of nitro compounds
    • C07C201/12Preparation of nitro compounds by reactions not involving the formation of nitro groups
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C45/00Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
    • C07C45/42Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by hydrolysis
    • C07C45/43Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by hydrolysis of >CX2 groups, X being halogen
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C47/00Compounds having —CHO groups
    • C07C47/52Compounds having —CHO groups bound to carbon atoms of six—membered aromatic rings
    • C07C47/544Diformyl benzenes; Alkylated derivatives thereof
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C47/00Compounds having —CHO groups
    • C07C47/52Compounds having —CHO groups bound to carbon atoms of six—membered aromatic rings
    • C07C47/56Compounds having —CHO groups bound to carbon atoms of six—membered aromatic rings containing hydroxy groups
    • C07C47/565Compounds having —CHO groups bound to carbon atoms of six—membered aromatic rings containing hydroxy groups all hydroxy groups bound to the ring
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/347Preparation of carboxylic acids or their salts, halides or anhydrides by reactions not involving formation of carboxyl groups
    • C07C51/373Preparation of carboxylic acids or their salts, halides or anhydrides by reactions not involving formation of carboxyl groups by introduction of functional groups containing oxygen only in doubly bound form

Definitions

  • the invention relates to a particularly advantageous process for the preparation of optionally substituted o-phthalaldehydes.
  • R 1 and / or R 2 are lower alkyl, they can be a straight or branched lower alkyl radical having 1-7 carbon atoms and are preferably methyl, ethyl, n-propyl and isopropyl, furthermore n-butyl, isobutyl, sec. Butyl, tert. Butyl, n-amyl, isoamyl, n-hexyl, isohexyl or n-heptyl.
  • R 1 and R 2 represent a halogen atom
  • halogen atoms up to atom number 35 such as fluorine, chlorine or bromine, are suitable. Chlorine or bromine are preferably suitable as the substituent X of the starting compound II.
  • Carboxylate is understood to mean the salt of an organic carboxylic acid, the salts being primarily metal, such as alkali metal or alkaline earth metal salts, furthermore ammonium salts of such acids, in particular of corresponding aliphatic, and also also aromatic carboxylic acids, such as of lower alkane carboxylic acids, for example of formic, Acetic or propionic acid, as well as benzoic acid. It is preferred to use alkali metal, such as sodium or potassium, and also calcium lower alkanoates with 1 to 3 carbon atoms, including the formates, in particular the corresponding formates and acetates, and primarily Sodium or potassium formate or acetate.
  • the phase transfer catalyst used is predominantly onium salts, in particular quaternary ammonium salts and phosphonium salts, for example tetraalkylammonium salts or phosphonium salts, in particular corresponding halides, such as tetra-n-butylammonium chloride or bromide or tetra-n-butylphosphonium chloride or bromide or ethyl bromide or ethyl bromide or ethyl bromide or ethyl bromide or ethyl bromide or ethyl bromide or ethyl bromide or ethyl bromide or ethyl bromide or ethyl bromide or ethyl bromide, ethyl trio or aryl-lower alkyl-tri-lower alkyl ammonium salts, in particular corresponding halides, for example Benzyltriethylammonium
  • a base is added to neutralize the acid corresponding to the carboxylate reagent which is formed in the hydrolysis of acylal intermediates and to accelerate this hydrolysis.
  • Inorganic bases such as corresponding metallic bases, e.g. Alkali metal or alkaline earth metal bases, in particular the corresponding hydroxides, hydrogen carbonates or preferably carbonates, such as sodium or potassium hydroxide or hydrogen carbonate, and preferably potassium or primarily sodium carbonate.
  • corresponding hydroxides, bicarbonate and carbonates of calcium or magnesium can be used in an analogous manner, calcium carbonate possibly being preferred as the poorly soluble base.
  • the reaction is usually carried out in a two-phase system, which consists of an aqueous and an organic phase, the latter from the ⁇ , ⁇ , ⁇ ', ⁇ '-tetrahslogene-o-xylene, for example from the a, a, ⁇ ' ⁇ '-Tetrabromo- or ⁇ , ⁇ , ⁇ ', ⁇ '-tetrachloro-x-xylene is formed.
  • Transfer catalyst compounds can vary considerably.
  • An inorganic base is added to the reaction mixture to neutralize the resulting acid, which converts it back into the carboxylate compound.
  • catalytic amounts ie less than equimolar amounts, for example from about 1 mole percent to about 50 mole percent (based on the starting material) of both the carboxylate and the phase transfer compound.
  • the latter are usually added in catalytic amounts, for example from about 1 mole percent to about 30 mole percent (based on the starting material), it also being possible to use equimolar amounts or an excess of the phase transfer catalyst.
  • the carboxylate compound is usually used in approximately equimolar amounts, if appropriate in a lower and preferably in an excess.
  • a readily soluble base such as an alkali metal carbonate, for example sodium carbonate, is preferably added in the course of the reaction, usually in portions.
  • reaction mixture is temporarily cooled before adding the base, for example in order to prevent foaming when using a carbonate or bicarbonate.
  • a poorly soluble base can also be present in the reaction mixture right from the start, which is why it is also preferably used, for example calcium carbonate.
  • the hydrolysis is carried out using a readily soluble base, for example an alkali metal base, preferably in a pH range from about 7.5 to about 11 and in the presence of a poorly soluble base, for example an alkaline earth metal carbonate, such as calcium carbonate, in a pH range below 7.5 executed; depending on the solubility of the alkaline earth carbonate used, the pH drops to about 4. Since the ⁇ , ⁇ , ⁇ ', ⁇ '-tetrabromo-o-xylene or ⁇ , ⁇ , ⁇ ', ⁇ '-tetrachloro-x-xylene as the starting material.
  • a readily soluble base for example an alkali metal base, preferably in a pH range from about 7.5 to about 11 and in the presence of a poorly soluble base, for example an alkaline earth metal carbonate, such as calcium carbonate, in a pH range below 7.5 executed; depending on the solubility of the alkaline earth carbonate used, the pH drops to about 4. Since the
  • the reaction becomes preferably at a temperature above 60 ° C, for example at a temperature of about 65 ° C to about 160 ° C, preferably from 90 ° C to about 140 ° C, further under normal pressure or elevated pressure, for example in a bomb tube or autoclave, and / or carried out under an inert gas atmosphere, for example nitrogen or argon.
  • the optionally substituted ⁇ , ⁇ , ⁇ ', ⁇ '-tetrabromo or ⁇ , ⁇ , ⁇ ', ⁇ '-tetrachloro-xylenes used as starting material are known and can e.g. by treating o-xylenes with elemental bromine while irradiating them with UV light (Organic Syntheses, Coll. Vol. IV, p. 807-808) or by treating o-xylenes with elemental chlorine while irradiating them with visible light (Houben-Weyl , Vol. 5/3, p. 739).
  • o-phthalaldehyde or optionally substituted o-phthalaldehyde which can be prepared according to the invention are used, for example, as a reagent for the qualitative and quantitative determination of ammonia or else primary amines (peptide chemistry). Secondary amines do not react with the o-phthalaldehydes.
  • the organic phase is separated off in a separating funnel and the aqueous phase is washed again with ethyl acetate.
  • the combined organic extracts (ethyl acetate extracts) are washed with a saline solution, dried over magnesium sulfate and then concentrated in vacuo.
  • the residue obtained is taken up in 40 ml of toluene and the solution is chromatographically purified on a column filled with silica gel (100 g). After evaporation of the eluate from toluene, 2.10 g (66.2% of theory) o -Phthalaldehyde, FP 53-55 °, can be isolated.
  • Example 2 Analogously to Example 1, a suspension consisting of 5.78 g of ⁇ , ⁇ , ⁇ ', ⁇ '-tetrachloroxylene (purity approx. 95%), 9.62 g of sodium acetate, 1.74 g of tetrabutylammonium bromide, 4.75 g of calcium carbonate and 10 ml of water are placed in a nitrogen atmosphere Stir cooked under reflux for 29 hours. After cooling, the mixture is diluted with water, extracted twice with ethyl acetate (100 ml each), the combined organic layers are washed with saturated sodium chloride solution and dried over magnesium sulfate.

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
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  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

Die vorliegende Erfindung betrifft ein Verfahren zur Herstellung von gegebenenfalls substituierten o-Phthalaldehydrn durch Hydrolyse von α,α,α',α'-Tetrahalogen-o-xylolen mit einem Carboxylat in wässrigem Medium in Gegenwart eines Phasentransferkatalysators und einer organischen Base.The present invention relates to a process for the preparation of optionally substituted o-phthalaldehydes by hydrolysis of α, α, α ', α'-tetrahalogen-o-xylenes with a carboxylate in an aqueous medium in the presence of a phase transfer catalyst and an organic base.

Description

Verfahren für die Herstellung von o-Phthalaldehyd sind in mehrfacher Weise in der Literatur schon seit langem beschrieben worden.Processes for the preparation of o-phthalaldehyde have long been described in the literature in a number of ways.

Zu erwähnen ist das in mehreren Stufen von J. Thiele und E. Winter, A 311, 360 (1900) verlaufende Oxydationsverfahren, welches von o-Xylol ausgehend Uber das Phthalaldehyd-tetraazetat verläuft. Die von F. Weygand und D. Tietjen in B 84, 625 (1951) beschriebene Methode liefert den o-Phthalaldehyd, wobei N,N,N',N'-Tetramethyl-o-phthalamid mittels Lithiumaluminiumhydrid als geeignetes Carbonsäurederivat reduziert wird. Eine Reduktion des verwendeten Tetramethyl-o-phthalamids kann nur unter peinlichstem Feuchtigkeitsausschluss ausgeführt werden, so dass erhebliche verfahrenstechnische Schwierigkeiten in Kauf genommen werden mUssen. Ein weiteres Verfahren gemäss F. Weygand, K.G. Kinkel und D. Tietjen in B 83, 394 (1950) geht vom o-Phthalalkohol aus. Die Oxydation des Alkohols erfolgt mit Selendioxid, wobei sich der Ester der selenigen Säure als Zwischenprodukt bildet, der erst durch vorsichtiges Erhitzen über offener Flamme zum Aldehyd umgewandelt wird. Bisher von Interesse war die durch J. Thiele und 0. Günther, A 347, 106 (1906) beschriebene Hydrolyse des α,α,α',α'-Tetrabrom-o-xylols mittels Kaliumoxalat. Als nachteilig erwies sich'die lange Reaktionszeit und die unbedingt notwendige Verwendung eines Lösungsgemisches aus Alkohol und Wasser in relativ grossen Volumenmengen. Auch die von F. Weygand et al., B 80, 391 (1947) beschriebene Hydrolyse des Tetrabrom-o-xylols kann als interessante Methode bezeichnet werden. Als nachteilig erweist sich jedoch hier die Verwendung von rauchender Schwefelsäure. Die durch Aufgiessen auf Eis erhaltene volumenmässig grosse Menge schwefelsaurer wässriger Lösung muss mit grossen Mengen Kochsalz gesättigt und mit grossen Volumenmengen an Essigester ausgeschüttelt werden. Obgleich der o-Phthalaldehyd schon lange zu den bekannten Substanzen gehört, fehlt auch heute noch eine einfache, d.h, unter Verwendung von billigen Ausgangsstoffen und Reagentien verlaufende und wenig Stufen beanspruchende Synthese zur Herstellung dieser Verbindung, die diese in guter Ausbeute ergibt.Worth mentioning is the oxidation process in several stages by J. Thiele and E. Winter, A 311, 360 (1900), which proceeds from o-xylene via phthalaldehyde tetraacetate. The method described by F. Weygand and D. Tietjen in B 84, 625 (1951) provides the o-phthalaldehyde, whereby N, N, N ', N'-tetramethyl-o-phthalamide is reduced by means of lithium aluminum hydride as a suitable carboxylic acid derivative. A reduction in the tetramethyl-o-phthalamide used can only be carried out with the most embarrassing exclusion of moisture, so that considerable procedural difficulties have to be accepted. Another method according to F. Weygand, KG Kinkel and D. Tietjen in B 83, 394 (1950) starts from o-phthalic alcohol. The alcohol is oxidized with selenium dioxide, whereby the ester of selenic acid forms as an intermediate product, which is only converted to aldehyde by careful heating over an open flame. So far, the one described by J. Thiele and 0. Günther, A 347, 106 (1906) has been of interest Hydrolysis of α, α, α ', α'-tetrabromo-o-xylene using potassium oxalate. The long reaction time and the absolutely necessary use of a solution mixture of alcohol and water in relatively large volumes proved to be disadvantageous. The hydrolysis of tetrabromo-o-xylene described by F. Weygand et al., B 80, 391 (1947) can also be described as an interesting method. However, the use of fuming sulfuric acid proves to be disadvantageous here. The large volume of sulfuric acid aqueous solution obtained by pouring it onto ice must be saturated with large amounts of sodium chloride and shaken out with large volumes of ethyl acetate. Although o-phthalaldehyde has long been one of the known substances, a simple synthesis, ie, using inexpensive starting materials and reagents and using little steps, is still missing to prepare this compound, which gives it in good yield.

Die Erfindung betrifft ein besonders vorteilhaftes Verfahren zur Herstellung von gegebenenfalls substituierten o-Phthalaldehyden.The invention relates to a particularly advantageous process for the preparation of optionally substituted o-phthalaldehydes.

Das erfindungsgemässe Verfahren zur Herstellung eines gegebenenfalls substituierten o-Phthalaldehyds der Formel I,

Figure imgb0001
in der R1 und R2 unabhängig voneinander Wasserstoff, Niederalkyl, Hydroxy, Halogen, Nitro, Cyano oder Carboxy bedeuten, besteht darin, dass man ein gegebenenfalls substituiertes α,α,α',α'-Tetrahalogen-o-xylol der Formel II,
Figure imgb0002
in der R1 und R2 die oben angegebene Bedeutung haben und X ein Halogenatom bedeutet mit einem Carboxylat in wässrigem Medium in Gegenwart eines Phasentransferkatalysators und einer anorganischen Base zum gegebenenfalls substituierten o-Phthalaldehyd hydrolysiert.The process according to the invention for the preparation of an optionally substituted o-phthalaldehyde of the formula I,
Figure imgb0001
in which R 1 and R 2 independently of one another are hydrogen, lower alkyl, hydroxy, halogen, nitro, cyano or carboxy mean that an optionally substituted α, α, α ', α'-tetrahalo-o-xylene of the formula II,
Figure imgb0002
in which R 1 and R 2 have the meaning given above and X denotes a halogen atom with a carboxylate in aqueous medium in the presence of a phase transfer catalyst and an inorganic base to hydrolyze the optionally substituted o-phthalaldehyde.

Falls R1 und/oder R2 Niederalkyl bedeuten, so können sie einen geraden oder verzweigten Niederalkylrest mit 1-7 Kohlenstoffatomen bedeuten und sind vorzugsweise Methyl, Aethyl, n-Propyl und Isopropyl, ferner n-Butyl, Isobutyl, sek. Butyl, tert. Butyl, n-Amyl, Isoamyl, n-Hexyl, Isohexyl oder n-Heptyl.If R 1 and / or R 2 are lower alkyl, they can be a straight or branched lower alkyl radical having 1-7 carbon atoms and are preferably methyl, ethyl, n-propyl and isopropyl, furthermore n-butyl, isobutyl, sec. Butyl, tert. Butyl, n-amyl, isoamyl, n-hexyl, isohexyl or n-heptyl.

Falls R1 und R2 ein Halogenatom bedeuten, so kommen als Halogenatome solche bis zur Atomnummer 35, wie z.B. Fluor, Chlor oder Brom in Betracht. Als Substituent X der Ausgangsverbindung II kommt vorzugsweise Chlor oder Brom in Betracht.If R 1 and R 2 represent a halogen atom, halogen atoms up to atom number 35, such as fluorine, chlorine or bromine, are suitable. Chlorine or bromine are preferably suitable as the substituent X of the starting compound II.

Unter Carboxylat wird das Salz einer organischen Carbonsäure verstanden, wobei als Salze in erster Linie Metall-, wie Alkalimetall- oder Erdalkalimetallsalze, ferner Ammoniumsalze von solchen Säuren, insbesondere von entsprechenden aliphatischen, ferner auch aromatischen Carbonsäuren, wie von Niederalkancarbonsäuren, z.B. von Ameisen-, Essig-oder Propionsäure, sowie von Benzoesäure in Frage kommen. Vorzugsweise verwendet man Alkalimetall-, wie Natrium- oder Kalium-, ferner auch Calciumniederalkanoate mit 1 bis 3 Kohlenstoffatomen unter Einbeziehung der Formiate, insbesondere die entsprechenden Formiate und Acetate und in erster Linie Natrium- oder Kaliumformiat oder -acetat.Carboxylate is understood to mean the salt of an organic carboxylic acid, the salts being primarily metal, such as alkali metal or alkaline earth metal salts, furthermore ammonium salts of such acids, in particular of corresponding aliphatic, and also also aromatic carboxylic acids, such as of lower alkane carboxylic acids, for example of formic, Acetic or propionic acid, as well as benzoic acid. It is preferred to use alkali metal, such as sodium or potassium, and also calcium lower alkanoates with 1 to 3 carbon atoms, including the formates, in particular the corresponding formates and acetates, and primarily Sodium or potassium formate or acetate.

Als Phasentransferkatalysator verwendet man vorwiegend Oniumsalze, insbesondere quaternäre Ammoniumsalze und Phosphoniumsalze, beispielsweise Tetraalkyl-ammoniumsalze bzw. -phosphoniumsalze, insbesondere entsprechende Halogenide, wie Tetra-n-butylammoniumchlorid oder -bromid bzw. Tetra-n-butylphosphoniumchlorid oder -bromid, Aethyltrioctylphosphoniumchlorid oder -bromid oder Arylniederalkyl-tri-niederalkylammoniumsalze, insbesondere entsprechende Halogenide, z.B. Benzyltriäthylammoniumchlorid. In analoger Weise können auch die entsprechenden Arsonium- und Sulfoniumsalze (E.V. Dehmlow, Ang. Chem. 89/8, 521-533) verwendet werden.The phase transfer catalyst used is predominantly onium salts, in particular quaternary ammonium salts and phosphonium salts, for example tetraalkylammonium salts or phosphonium salts, in particular corresponding halides, such as tetra-n-butylammonium chloride or bromide or tetra-n-butylphosphonium chloride or bromide or ethyl bromide or ethyl bromide or ethyl bromide or ethyl bromide or ethyl bromide or ethyl bromide or ethyl bromide or ethyl bromide, ethyl trio or aryl-lower alkyl-tri-lower alkyl ammonium salts, in particular corresponding halides, for example Benzyltriethylammonium chloride. The corresponding arsonium and sulfonium salts (E.V. Dehmlow, Ang. Chem. 89/8, 521-533) can also be used in an analogous manner.

Zur Neutralisierung der dem Carboxylatreagens entsprechenden Säure, die bei der Hydrolyse von Acylalzwischenprodukten entsteht, und zur Beschleunigung dieser Hydrolyse wird eine Base zugegeben. Man verwendet üblicherweise anorganische Basen, wie entsprechende metallische Basen, z.B. Alkalimetall- oder Erdalkalimetallbasen, insbesondere die entsprechenden Hydroxide, Hydrogencarbonate oder vorzugsweise Carbonate, wie Natrium- oder Kaliumhydroxyd oder -hydrogencarbonat, und vorzugsweise Kalium- oder in erster Linie Natriumcarbonat. In analoger Weise können die entsprechenden Hydroxide, Hydrogencarbonat und Carbonate des Calciums oder Magnesiums verwendet werden, wobei Calciumcarbonat als schwerlösliche Base gegebenenfalls bevorzugt sein kann.A base is added to neutralize the acid corresponding to the carboxylate reagent which is formed in the hydrolysis of acylal intermediates and to accelerate this hydrolysis. Inorganic bases, such as corresponding metallic bases, e.g. Alkali metal or alkaline earth metal bases, in particular the corresponding hydroxides, hydrogen carbonates or preferably carbonates, such as sodium or potassium hydroxide or hydrogen carbonate, and preferably potassium or primarily sodium carbonate. The corresponding hydroxides, bicarbonate and carbonates of calcium or magnesium can be used in an analogous manner, calcium carbonate possibly being preferred as the poorly soluble base.

Die Reaktion wird Ublicherweise in einem zweiphasigen System durchgeführt, das aus einer wässrigen und einer organischen Phase besteht, wobei letztere aus dem α,α,α',α'-Tetrahslogen-o-xylol, beispielsweise aus dem a,a, α'α'-Tetrabrom- oder α,α,α',α'-Tetrachlor-o-xylol gebildet wird. Die erfindungsgemäss einzusetzenden Mengen der Carboxylat- und Phasentransferkatalysator-Verbindungen können erheblich variieren. Dem Reaktionsgemisch gibt man eine anorganische Base zur Neutralisierung der entstehenden Säure bei, die diese wieder in die Carboxylat-Verbindung überführt. Man könnte theoretisch katalytische Mengen, d.h. weniger als äquimolare Mengen, z.B. von etwa 1 Molprozent bis etwa 50 Molprozent (bezogen auf das Ausgangsmaterial) sowohl der Carboxylat-,.als auch der Phasentransfer-Verbindung verwenden. Ueblicherweise gibt man letztere in katalytischen Mengen, z.B. von etwa 1 Molprozent bis etwa 30 Molprozent (bezogen auf das Ausgangsmaterial) zu, wobei auch äquimolare Mengen oder ein Ueberschuss des Phasentransferkatalysators verwendet werden können. Die Carboxylatverbindung wird üblicherweise in etwa äquimolaren Mengen, gegebenenfalls in einem Unter-, und vorzugsweise in einem Ueberschuss angewandt. Vorzugsweise wird eine leicht-lösliche Base, wie ein Alkalimetallcarbonat, z.B. Natriumcarbonat, im Verlauf der Reaktion, üblicherweise in Portionen zugegeben. Falls notwendig, wird dabei das Reaktionsgemisch vor Zugabe der Base vorübergehend abgekühlt, z.B. um bei Verwendung eines Carbonats oder Hydrogencarbonats ein Ueberschäumen zu verhindern. Eine schwerlösliche Base kann jedoch auch von Anfang an im Reaktionsgemisch vorliegen, weshalb diese auch bevorzugt, beispielsweise Calciumcarbonat, verwendet wird.The reaction is usually carried out in a two-phase system, which consists of an aqueous and an organic phase, the latter from the α, α, α ', α'-tetrahslogene-o-xylene, for example from the a, a, α'α '-Tetrabromo- or α, α, α', α'-tetrachloro-x-xylene is formed. The amounts of the carboxylate and phases to be used according to the invention Transfer catalyst compounds can vary considerably. An inorganic base is added to the reaction mixture to neutralize the resulting acid, which converts it back into the carboxylate compound. In theory, one could use catalytic amounts, ie less than equimolar amounts, for example from about 1 mole percent to about 50 mole percent (based on the starting material) of both the carboxylate and the phase transfer compound. The latter are usually added in catalytic amounts, for example from about 1 mole percent to about 30 mole percent (based on the starting material), it also being possible to use equimolar amounts or an excess of the phase transfer catalyst. The carboxylate compound is usually used in approximately equimolar amounts, if appropriate in a lower and preferably in an excess. A readily soluble base, such as an alkali metal carbonate, for example sodium carbonate, is preferably added in the course of the reaction, usually in portions. If necessary, the reaction mixture is temporarily cooled before adding the base, for example in order to prevent foaming when using a carbonate or bicarbonate. However, a poorly soluble base can also be present in the reaction mixture right from the start, which is why it is also preferably used, for example calcium carbonate.

Die Hydrolyse wird bei Verwendung einer leicht löslichen Base, beispielsweise einer Alkalimetallbase, vorzugsweise in einem pH-Bereich von etwa 7,5 bis etwa 11 und in Gegenwart einer schwer löslichen Base, beispielsweise eines Erdalkalicarbonates, wie z.B. Calciumcarbonat, in einem pH-Bereich unterhalb 7,5 ausgefuhrt; der pH-Wert sinkt je nach Löslichkeit des verwendeten Erdalkalicarbonates bis auf etwa 4.
Da das α,α,α',α'-Tetrabrom-o-xylol oder α,α,α',α'-Tetrachlor- o-xylol als Ausgangsmaterial.in geschmolzenem Zustand die organische Phase des zweiphasen Systems bildet, wird die Reaktion vorzugsweise bei einer Temperatur oberhalb von 60° C, z.B. bei einer Temperatur von etwa 65°C bis etwa 160°C, vorzugsweise von 90° C bis etwa 140° C, ferner unter Normaldruck oder erhöhtem Druck, z.B. im Bombenrohr oder Autoklaven, und/oder unter einer Inertgasatmosphäre, z.B. Stickstoff oder Argon, durchgeführt.
The hydrolysis is carried out using a readily soluble base, for example an alkali metal base, preferably in a pH range from about 7.5 to about 11 and in the presence of a poorly soluble base, for example an alkaline earth metal carbonate, such as calcium carbonate, in a pH range below 7.5 executed; depending on the solubility of the alkaline earth carbonate used, the pH drops to about 4.
Since the α, α, α ', α'-tetrabromo-o-xylene or α, α, α', α'-tetrachloro-x-xylene as the starting material. In the molten state forms the organic phase of the two-phase system, the reaction becomes preferably at a temperature above 60 ° C, for example at a temperature of about 65 ° C to about 160 ° C, preferably from 90 ° C to about 140 ° C, further under normal pressure or elevated pressure, for example in a bomb tube or autoclave, and / or carried out under an inert gas atmosphere, for example nitrogen or argon.

Die als Ausgangsmaterial verwendeten gegebenenfalls substituierten α,α,α',α'-Tetrabrom- oder α,α,α',α'-Tetrachlor-o-xylole sind bekannt und können z.B. durch Behandeln von o-Xylolen mit elementarem Brom unter Bestrahlen mit UV-Licht (Organic Syntheses, Coll. Vol. IV, p. 807-808) oder durch Behandeln von o-Xylolen mit elementarem Chlor unter Bestrahlung mit sichtbarem Licht (Houben-Weyl, Bd. 5/3, S. 739) hergestellt werden.The optionally substituted α, α, α ', α'-tetrabromo or α, α, α', α'-tetrachloro-xylenes used as starting material are known and can e.g. by treating o-xylenes with elemental bromine while irradiating them with UV light (Organic Syntheses, Coll. Vol. IV, p. 807-808) or by treating o-xylenes with elemental chlorine while irradiating them with visible light (Houben-Weyl , Vol. 5/3, p. 739).

Im Vergleich zum nächstliegenden Stand der Technik, d.h. im Vergleich zu dem von F. Weygand et al., B 80, 391 (1947) beschriebenen Verfahren wird die Hydrolyse ohne rauchende Schwefelsäure ausgeführt. Die hierbei anfallende, mit Kochsalz gesättigte, grosse Menge wässriger Lösung muss wiederum mit einer volumenmässig grossen Menge Essigester als Lösungsmittel ausgeschüttelt werden. Diese verfahrensmässigen Nachteile liegen beim erfindungsgemäss ausführbaren Verfahren nicht vor.Compared to the closest prior art, i.e. compared to the process described by F. Weygand et al., B 80, 391 (1947), the hydrolysis is carried out without fuming sulfuric acid. The resulting large amount of aqueous solution saturated with common salt must in turn be shaken out with a large volume of ethyl acetate as the solvent. These procedural disadvantages do not exist in the method which can be carried out according to the invention.

Der erfindungsgemäss herstellbare o-Phthalaldehyd bzw. gegebenenfalls substituierte o-Phthalaldehyde werden beispielsweise als Reagens für die qualitative und quantitative Bestimmung von Ammoniak oder auch primären Aminen (Peptidchemie) verwendet. Sekundäre Amine reagieren mit den o-Phthalaldehyden nicht.The o-phthalaldehyde or optionally substituted o-phthalaldehyde which can be prepared according to the invention are used, for example, as a reagent for the qualitative and quantitative determination of ammonia or else primary amines (peptide chemistry). Secondary amines do not react with the o-phthalaldehydes.

· In den nachfolgenden Beispielen werden die Temperaturen in Celsiusgraden angegeben.· In the following examples, the temperatures are given in degrees Celsius.

Beispiel 1example 1

Eine Suspension bestehend aus 10,0 g α,α,α',α'-Tetrabrom-o-xylol (23,7 mMol), 9,7 g Natriumazetat (118 mMol), 1,74 g Tetrabutylammoniumbromid (5,4 mMol), 4,75 g Calciumcarbonat und 10 ml destilliertem Wasser wird in einer Stickstoffatmosphäre unter kräftigem Rühren zum RUckfluss erhitzt, wobei sich die Innentemperatur auf 118° einstellt. Nach 6-stündiger Reaktionsdauer lässt man das Reaktionsgemisch abkühlen, fügt 50 ml Essigester hinzu und filtriert. Im Scheidetrichter wird die organische Phase abgetrennt und die wässrige Phase nochmals mit Essigester gewaschen. Die vereinigten organischen Auszüge (Essigesterextrakte) werden mit einer Kochsalzlösung gewaschen, Uber Magnesiumsulfat getrocknet und anschliessend im Vakuum eingeengt. Der erhaltene Rückstand wird in 40 ml Toluol aufgenommen und die Lösung an einer Säule, gefüllt mit Silicagel (100 g), chromatographisch gereinigt, wobei nach dem Eindampfen des Eluates aus Toluol 2,10 g (66,2 % d.Th.) o-Phthalaldehyd, F.P. 53-55°, isoliert werden.A suspension consisting of 10.0 g α, α, α ', α'-tetrabromo-o-xylene (23.7 mmol), 9.7 g sodium acetate (118 mmol), 1.74 g tetrabutylammonium bromide (5.4 mmol ), 4.75 g of calcium carbonate and 10 ml of distilled water is heated to reflux in a nitrogen atmosphere with vigorous stirring, the internal temperature adjusting to 118 °. After a reaction time of 6 hours, the reaction mixture is allowed to cool, 50 ml of ethyl acetate are added and the mixture is filtered. The organic phase is separated off in a separating funnel and the aqueous phase is washed again with ethyl acetate. The combined organic extracts (ethyl acetate extracts) are washed with a saline solution, dried over magnesium sulfate and then concentrated in vacuo. The residue obtained is taken up in 40 ml of toluene and the solution is chromatographically purified on a column filled with silica gel (100 g). After evaporation of the eluate from toluene, 2.10 g (66.2% of theory) o -Phthalaldehyde, FP 53-55 °, can be isolated.

Beispiel 2Example 2

Eine Suspension bestehend aus 10,0 g α,α,α',α'- Tetrabrom-o-xylol. 8,0 g Natriumformiat, 1,74 g Tetrabutyl- ammoniumbromid, 4,75 g Calciumcarbonat und 10 ml destilliertem Wasser wird in einer Stickstoffatmosphäre unter kräftigem Rühren 9 Stunden lang unter RUckfluss erhitzt. Nach dem Abkühlen werden 50 ml Essigester hinzugefügt. und das Reaktionsgemisch wie unter Beispiel 1 weiterverarbeitet. Nach chromatographischer Reinigung (100 g Silicagel in der Säule) werden 2,54 g o-Phthalaldehyd (80.2% d.Th.), F.P. 53-55°, isoliert.A suspension consisting of 10.0 g of α, α, α ', α'-tetrabromo-o-xylene. 8.0 g of sodium formate, 1.74 g of tetrabutylammonium bromide, 4.75 g of calcium carbonate and 10 ml of distilled water are refluxed in a nitrogen atmosphere with vigorous stirring for 9 hours. After cooling, 50 ml of ethyl acetate are added. and the reaction mixture processed as in Example 1. After chromatographic purification (100 g silica gel in the column), 2.54 g o-phthalaldehyde (80.2% of theory), F.P. 53-55 °, isolated.

Beispiel 3Example 3

In Analogie zu Beispiel 1 wird eine Suspension bestehend aus 5.78 g α,α,α',α'-Tetrachlorxylol (Reinheit ca. 95%), 9.62 g Natriumacetat, 1.74 g Tetrabutylammoniumbromid, 4.75 g Calciumcarbonat und 10 ml Wasser in einer Stickstoffatmosphäre unter Rühren 29 Stunden unter RUckfluss gekocht. Nach dem Abkühlen wird mit Wasser verdünnt, mit Essigester zweimal (je 100 ml) extrahiert, die vereinigten organischen Schichten mit gesättigter Kochsalzlösung gewaschen und über Magnesiumsulfat getrocknet. Das Lösungsmittel wird im Vakuum abdestilliert und der kristalline Rückstand in Toluol gelöst und an 100 g Silicagel chromatographiert. o-Phthaldialdehyd wird mit Toluol Essigester = 19:1 eluiert, wobei nach dem Eindampfen des Eluates 2.30 g (72% d.Th.) gereinigter o-Phthalaldehyd erhalten werden.Analogously to Example 1, a suspension consisting of 5.78 g of α, α, α ', α'-tetrachloroxylene (purity approx. 95%), 9.62 g of sodium acetate, 1.74 g of tetrabutylammonium bromide, 4.75 g of calcium carbonate and 10 ml of water are placed in a nitrogen atmosphere Stir cooked under reflux for 29 hours. After cooling, the mixture is diluted with water, extracted twice with ethyl acetate (100 ml each), the combined organic layers are washed with saturated sodium chloride solution and dried over magnesium sulfate. The solvent is distilled off in vacuo and the crystalline residue is dissolved in toluene and chromatographed on 100 g of silica gel. o-Phthalaldehyde is eluted with toluene ethyl acetate = 19: 1, whereby after evaporation of the eluate 2.30 g (72% of theory) of purified o-phthalaldehyde are obtained.

Claims (11)

1. Verfahren zur Herstellung eines gegebenenfalls substituierten o-Phthalaldehyds der Formel I,
Figure imgb0003
in der R1 und R2 unabhängig voneinander Wasserstoff, Niederalkyl, Hydroxy, Halogen, Nitro, Cyano oder Carboxy bedeuten, dadurch gekennzeichnet, dass man ein gegebenenfalls substituiertes α,α,α',α'-Tetrahalogen-o-xylol der Formel II,
Figure imgb0004
in der R1 und R2 die oben angegebene Bedeutung haben und X ein Halogenatom bedeutet mit einem Carboxylat in wässrigem Medium in Gegenwart eines Phasentransferkatalysators und einer organischen Base hydrolysiert.
1. Process for the preparation of an optionally substituted o-phthalaldehyde of the formula I,
Figure imgb0003
in which R 1 and R 2 are independently hydrogen, lower alkyl, hydroxy, halogen, nitro, cyano or carboxy, characterized in that an optionally substituted α, α, α ', α'-tetrahalo-o-xylene of the formula II ,
Figure imgb0004
in which R 1 and R 2 have the meaning given above and X denotes a halogen atom with a carboxylate in aqueous medium in the presence of a phase transfer catalyst and an organic base.
2. Verfahren nach Patentanspruch 1, dadurch gekennzeichnet, dass man die Hydrolyse in Gegenwart eines quaternären Ammoniumsalzes oder Phosphoniumsalzes als Phasentransferkatalysator und einer metallischen Base, mit einem Alkali-, Erdalkali- oder Ammoniumsalz einer organischen Säure ausführt.2. The method according to claim 1, characterized in that one carries out the hydrolysis in the presence of a quaternary ammonium salt or phosphonium salt as a phase transfer catalyst and a metallic base, with an alkali metal, alkaline earth metal or ammonium salt of an organic acid. 3. Verfahren nach Patentanspruch 1 oder 2, dadurch gekennzeichnet, dass man die Hydrolyse in Gegenwart eines Tetraniederalkylammoniunsalzes und einer Alkalimetall-oder Erdalkalimetallbase mit einem Alkali-, Erdalkali-oder Ammoniumsalz einer aliphatischen Carbonsäure, wie einer Niederalkancarbonsäure oder einer aromatischen Carbonsäure ausführt.3. The method according to claim 1 or 2, characterized in that one carries out the hydrolysis in the presence of a tetraniederalkylammoniunsalzes and an alkali metal or alkaline earth metal base with an alkali, alkaline earth or ammonium salt of an aliphatic carboxylic acid, such as a lower alkane carboxylic acid or an aromatic carboxylic acid. 4. Verfahren nach einem der Patentansprüche 1 bis 3, dadurch gekennzeichnet, dass man die Hydrolyse in Gegenwart von Tetra-n-butylammoniumchlorid oder -bromid als Phasentransferkatalysator und eines Alkalimetall- oder Erdalkalimetallcarbonates mit einem Alkalimetall- oder Erdalkalimetallformiat oder -acetat ausführt.4. The method according to any one of claims 1 to 3, characterized in that one carries out the hydrolysis in the presence of tetra-n-butylammonium chloride or bromide as phase transfer catalyst and an alkali metal or alkaline earth metal carbonate with an alkali metal or alkaline earth metal formate or acetate. 5. Verfahren nach Patentanspruch 1 oder 2, dadurch gekennzeichnet, dass man die Hydrolyse in Gegenwart von Benzyltriäthylammoniumchlorid oder -bromid und eines Alkalimetall- oder Erdalkalimetallcarbonates mit einem Alkalimetall- oder Erdalkalimetallformiat oder -acetat ausführt.5. The method according to claim 1 or 2, characterized in that one carries out the hydrolysis in the presence of benzyltriethylammonium chloride or bromide and an alkali metal or alkaline earth metal carbonate with an alkali metal or alkaline earth metal formate or acetate. 6. Verfahren nach einem der Patentansprüche 1 bis 4, dadurch gekennzeichnet, dass man die Hydrolyse in Gegenwart von Tetra-n-butylammoniumchlorid oder -bromid und Calciumcarbonat mit Natriumformiat oder -acetat ausführt.6. The method according to any one of claims 1 to 4, characterized in that one carries out the hydrolysis in the presence of tetra-n-butylammonium chloride or bromide and calcium carbonate with sodium formate or acetate. 7. Verfahren nach einem der Patentansprüche 1 bis 6, dadurch gekennzeichnet, dass man in Abwesenheit eines organischen Lösungsmittels bei einer Temperatur über 60° arbeitet.7. The method according to any one of claims 1 to 6, characterized in that one works in the absence of an organic solvent at a temperature above 60 °. 8. Verfahren nach einem der Patentansprüche 1 bis 7, dadurch gekennzeichnet, dass man als gegebenenfalls substituiertes a,a,a',a'-Tetrahalogen-o-xylol der Formel II ein gegebenenfalls substituiertes a,a,a',a'-Tetrabrom-oder α,α,α',α'-Tetrachlor-o-xylol verwendet.8. The method according to any one of claims 1 to 7, characterized in that an optionally substituted a, a, a ', a'- as optionally substituted a, a, a', a'-tetrahalo-o-xylene of the formula II Tetrabromo or α, α, α ', α'-tetrachloro-xylene used. 9. Das in den Beispielen 1 bis 3 beschriebene Verfahren.9. The procedure described in Examples 1 to 3. 10. Die nach dem Verfahren der Ansprüche 1 bis 8 erhältlichen Verbindungen.10. The compounds obtainable by the process of claims 1 to 8. 11. Die nach dem Verfahren der Beispiele 1 bis 3 erhältlichen Verbindungen.11. The compounds obtainable by the process of Examples 1 to 3.
EP78101723A 1977-12-30 1978-12-16 Process for the preparation of o-phthalic aldehydes optionally having several substituents Expired EP0003230B1 (en)

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EP0026291A1 (en) * 1979-08-28 1981-04-08 Hüls Troisdorf Aktiengesellschaft Process for the preparation of terephthalaldehyde or isophthalaldehyde
US7858381B2 (en) 2005-06-28 2010-12-28 Dsm Fine Chemicals Austria Nfg Gmbh & Co Kg Process for preparing high-purity, halogen-free o-phthaladehyde

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US4820829A (en) * 1986-01-16 1989-04-11 Ciba-Geigy Corporation Substituted o-phthalaldehydes
US4845305A (en) * 1988-07-07 1989-07-04 National Starch And Chemical Corporation Process for the preparation of isophthaladehyde
US5107032A (en) * 1990-11-20 1992-04-21 Noramco, Inc. Process for the preparation of o-phthalaldehydes
US6891069B1 (en) * 2004-01-30 2005-05-10 Ethicon, Inc. Synthesis of 4-substituted phthalaldehyde
CN114524718B (en) * 2022-01-25 2023-09-22 上海巽田科技股份有限公司 Method for preparing high-purity phthalic dicarboxaldehyde from phthalic diester

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US4125561A (en) * 1972-04-13 1978-11-14 Dynamit Nobel Aktiengesellschaft Process for production of terephthalic dialdehyde
US4079075A (en) * 1975-11-06 1978-03-14 The Dow Chemical Company Primary alkyl esters as mediums for oxidations by phase-transfer catalyzed hypohalites

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0026291A1 (en) * 1979-08-28 1981-04-08 Hüls Troisdorf Aktiengesellschaft Process for the preparation of terephthalaldehyde or isophthalaldehyde
US7858381B2 (en) 2005-06-28 2010-12-28 Dsm Fine Chemicals Austria Nfg Gmbh & Co Kg Process for preparing high-purity, halogen-free o-phthaladehyde

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